In a Danfoss CH scroll compressor, the
compression is performed by two scroll elements
located in the upper part of the compressor.
Suction gas enters the compressor at the suction
connection. As all of the gas flows around and
through the electrical motor, thus ensuring
complete motor cooling in all applications, oil
droplets separate and fall into the oil sump.
After exiting the electrical motor, the gas enters
the scroll elements where compression takes
place. Ultimately, the discharge gas leaves the
compressor at the discharge connection.
The figure below illustrates the entire
compression process. The centre of the orbiting
scroll (in grey) traces a circular path around
the centre of the fixed scroll (in black). This
movement creates symmetrical compression
pockets between the two scroll elements.
Low-pressure suction gas is trapped within
each crescent-shaped pocket as it gets formed;
continuous motion of the orbiting scroll serves
to seal the pocket, which decreases in volume
as the pocket moves towards the center of the
scroll set increasing the gas pressure. Maximum
compression is achieved once a pocket reaches
the center where the discharge port is located;
this stage occurs after three complete orbits.
Compression is a continuous process: the
scroll movement is suction, compression and
discharge all at the same time.
SUCTION
COMPRESSION
DISCHARGE
4FRCC.PC.026.A4.02
Application Guidelines
Features
CH range is composed of CH290 & CH485 (large
commercial platform).
Heat shield that lowers the heat
transfer between discharge and
suction gas and the acoustic level
R410A optimized and dedicated
scroll profile
Liquid slug protection per suction
fitting in upper position
5FRCC.PC.026.A4.02
Application Guidelines
Compressor model designation
Nomenclature
Family, lubricant
& refrigerant
CH: Scroll, POE lubricant, or R410A
Nominal capacity
in thousand Btu/h at 60 Hz, R410A,
ARI conditions
UL index
Motor voltage code
4: 380-415V/3~/50 Hz
Danfoss CH290 & CH485 scroll compressor
for R410A are available as single compressor.
The example below presents the compressor
nomenclature which equals the technical
Family,
lubricant
& refrigerant
Nominal
capacity
ApprovalsVoltageVersionEvolution
reference as shown on the compressor
nameplate. Code numbers for ordering are listed
section “Ordering information and packaging”.
index
A4CHABB290
Evolution index
A~Z
Motor protection
A: Electronic module, 24V AC
B: Electronic module, 115/240V
Suction and discharge connections
A: Brazed connections
B: Brazed, No oil sight glass, No oil equalization
TR: Ton of Refrigeration, Standard rating conditions: ARI standard Evaporating temperature: 7.2 °C Superheat: 11.1 K
EER: Energy Efficiency Ratio Refrigerant: R410A Condensing temperature: 54.4 °C Subcooling: 8.3 K
COP: Coefficient Of Performance,
Subject to modification without prior notification.
kg
7FRCC.PC.026.A4.02
Application Guidelines
CH290
Ø 257.4
Suction
1"5/8
Dimensions
Ø 265.9
Discharge: 1"1/8
653
618
370.8
301.5
304.8
170
195
60°
345.4
279.4
212
187
531.5 ± 1.2
Ø 318
214
All dimensions in mm
4 Holes
Ø 19
428
109
8FRCC.PC.026.A4.02
Flexible grommet
HM 8 bolt
Lock washer
Flat washer
Steel mounting sleeve
Rubber grommet
Nut
Compressor
base plate
27.5 mm
Application Guidelines
CH290 - Parallel version
Ø257.4
Dimensions
Ø265.9
Discharge
1"1/8
370.8
187
214
4x rigid
spacer 29.5
304.8
301.5
195
170
Ø317.5
345.4
279.4
183
76.6
60°
531.5
92.5
4x holes Ø19
428
Suction
1"5/8
All dimensions in mm
618
653
60°
212
353
109
Rigid spacer
29.5 mm
HM 8 bolt
Lock washer
Nut
Flat washer
Rigid spacer
Nut
9FRCC.PC.026.A4.02
Application Guidelines
CH485
Dimensions
Ø333.2
Ø318.1
Discharge:
SH485: 1"3/8
370.8
187
214
304.8
301.5
218.6
195
345.4
279.4
183
76.6
60°
524.8
92.5
4 holes Ø19
428
Suction
1"5/8
725.8
667
All dimensions in mm
10FRCC.PC.026.A4.02
60°
Rigid spacer
212
356
29.5 mm
109
HM 8 bolt
Lock washer
Nut
Flat washer
Rigid spacer
Nut
Flexible grommet
HM 8 bolt
Lock washer
Flat washer
Steel mounting sleeve
Rubber grommet
Nut
Compressor
base plate
27.5 mm
Application Guidelines
Dimensions
Suction and discharge
Connections
CH290
CH485
Brazed version
Tube ODF
Brazed
Suction1"5/8
Discharge1"1/8
Suction1"5/8
Discharge1"3/8
11FRCC.PC.026.A4.02
Application Guidelines
Electrical data, connections and wiring
Connection details
(Versions dedicated for
parallel mounting only)
CH290 & 485
VersionAA - AB
Suction and discharge connectionsBrazed
Oil sight glass Threaded
Oil equalisation connectionrotolock 2"1/4
Oil drain connection1/4" flare
Low pressure gauge port (schrader)1/4" flare
Danfoss CH290-485 scroll compressors are available with the motor voltage code 4:Motor voltage
Motor voltage codeCode 4
Nominal voltage380-415V - 3ph
50 Hz
Voltage range342-457V
12FRCC.PC.026.A4.02
Module power
Application Guidelines
Electrical data, connections and wiring
Wiring connections
Electrical power is connected to the compressor
terminals by Ø 4.8 mm (3/16") screws.
The terminal box is provided with 2 triple
knockouts and 1 single knockout for power
supply and 4 double knockouts for the safety
control circuit.
The 3 power supply knockouts accommodate the
following diameters:
• Ø 50.8 mm (UL 1"1/2 conduit) and Ø 43.7
mm (UL 1"1/4 conduit) and Ø 34.5 mm (UL 1"
conduit)
• Ø 40.5 mm (ISO40) and Ø 32.2 mm (ISO32) and
Ø 25.5 mm (ISO25)
• Ø 25.5 mm (ISO25)
The 4 others knockouts are as follows:
• Ø 22.5 mm (PG16) (UL 1/2") and Ø 16.5 mm
(ISO16) (x2)
• 20.7 mm (ISO20 or PG13.5) (x2)
The motor protection module comes preinstalled
within the terminal box. Phase sequence
protection connections and thermistor
connections are pre-wired and should not be
deinstalled. The module must be connected to
a power supply of the appropriate voltage. The
module terminals are 6.3-mm size Faston type.
The maximum tightening torque is 3 Nm. Use a
1/4’’ ring terminal on the power leads.
BlackBlueBrown
M1-M2
Control circuit
Module
power supply
Sump heater
Faston 1/4" tabs
Power supply
Phase sequence input
L1 L2 L3
Black Blue Brown
LNS1 S2 M1 M2
Internal control contact
Safety
Thermistor
connection
circuit
IP rating
Terminal box temperature
The compressor terminal box according to IEC529 is IP54 when correctly sized IP54 rated cable glands
are used.
First numeral, level of protection against contact and foreign objects
5 - Dust protected
Second numeral, level of protection against water
4 - Protection against water splashing
The temperature inside the terminal box may not
exceed 70°C. Consequently, if the compressor is
installed in an enclosure, precautions must be
taken to avoid that the temperature around the
compressor and in the terminal box would rise
too much. The installation of ventilation on the
electronic protection module may not operate
properly. Any compressor damage related to this
will not be covered by Danfoss warranty. In the
same manner, cables must be selected in a way
to insure that terminal box temperature does not
exceed 70°C.
enclosure panels may be necessary. If not, the
13FRCC.PC.026.A4.02
Application Guidelines
Electrical data, connections and wiring
Three phase electrical
characteristics
LRA (Locked Rotor Amp)
MCC (Maximum
Continuous Current)
Max. Operating Current.
Winding resistance
Compressor model
CH29026062560.52
Motor voltage code 4
CH48541390890.23
LRAMCCMax. operating currentWinding resistance
AAAΩ
Locked Rotor Amp value is the higher average
current as measured on mechanically blocked
compressor tested under nominal voltage. The
LRA value can be used as rough estimation for
The MCC is the current at which the motor
protection trips under maximum load and
low voltage conditions. This MCC value is the
maximum at which the compressor can be
operated in transient conditions and out of
The max. operating current is the current when
the compressors operate at maximum load
conditions and 10% below nominal voltage
(+15°C evaporating temperature and +68°C
Winding resistance is the resistance between
phases at 25°C (resistance value +/- 7%).
Winding resistance is generally low and it
requires adapted tools for precise measurement.
Use a digital ohm-meter, a “4 wires” method and
measure under stabilised ambient temperature.
Winding resistance varies strongly with winding
temperature. If the compressor is stabilised
at a different value than 25°C, the measured
resistance must be corrected using following
formula:
the starting current. However in most cases, the
real starting current will be lower. A soft starter
can be applied to reduce starting current.
the application envelope. Above this value, the
internal motor protection or external electronic
module will cut-out the compressor to protect
the motor.
condensing temperature). Max Oper. A can be
used to select cables and contactors. In normal
operation, the compressor current consumption
is always less than the Max Oper. A. value.
a + t
R
= R
tamb
25°C
a + t
t
: reference temperature = 25°C
25°C
t
: temperature during measurement (°C)
amb
R
: winding resistance at 25°C
25°C
R
: winding resistance at tamb
amb
amb
_______
25°C
Coefficient a = 234.5
General wiring
information
The wiring diagrams below are examples for a
safe and reliable compressor wiring. In case an
alternative wiring logic is chosen, it is imperative
to respect the following rules:
When a safety switch trips, the compressor must
stop immediately and must not re-start until
the tripping condition is back to normal and
the safety switch is closed again. This applies to
the LP safety switch, the HP safety switch, the
discharge gas thermostat and the motor safety
thermostat.
In specific situations, such as winter start
operation, an eventual LP control for pumpdown cycles may be temporarily bypassed to
allow the system to build pressure. But it remains
mandatory for compressor protection to apply an
LP safety switch. The LP safety switch must never
be bypassed.
Pressure settings for the LP and HP safety switch
and pump-down listed in table from section “Low
pressure”.
When ever possible (ie. PLC control), it is
recommended to limit the possibilities of
compressor auto restart to less than 3 to 5 times
during a period of 12 hours when caused by
motor protection or LP safety switch tripping.
This control must be managed as a manual reset
device.
14FRCC.PC.026.A4.02
Application Guidelines
Electrical data, connections and wiring
Danfoss MCI soft-start
controller
The inrush current for the CH scroll compressors
with motor 380-415V / 3ph / 50Hz can be
reduced using the Danfoss digitally-controlled
MCI compressor soft starter. MCI & MCD soft
starters are designed to reduce the starting
current of 3-phase AC motors; they can reduce
the inrush current by up to 40%, thereby
eliminating the detrimental effects of high
starting torque surges and costly demand
charges from the resultant current spike. Upon
starting, the controller gradually increases
the voltage supplied to the motor until fullline voltage has been reached. All settings,
such as ramp-up time (less than 0.5 sec) and
initial torque, are preset and do not require
modification.
Compressor model
CH290MCI50CM *MCI50CM *
CH485MCD201-055MCD201-055
* by-pass contactor K1 is required
Soft start reference
Ambient max. 40°C
Upon starting, the controller gradually increases
the voltage supplied to the motor until full-line
voltage has been reached.
For MCI50M, all settings such as initial torque,
ramp-up time (less than 0.5 sec) and rampdown time are preset and do not require any
modification.
When the control voltage is applied, the
MCI50CM soft starter will start the motor,
according to the settings of the ramp-up time
and initial torque adjustments. When the control
voltage is switched OFF, the motor will switch off
instantaneously.
On CH compressors, by pass contactor K1 is
required by means of the built-in auxiliary
contact (23-24) the by-pass function is easily
achieved, see wiring diagram beside.
No heat is generated from the MCI. As the
contactor always switches in no-load condition
it can be selected on the basis of the thermal
current (AC-1).
Soft start reference
Ambient max. 55°C
For MCD201-055, the following settings have to
be adjusted to ensure a maximum inrush current
reduction as well as a starting time less than
0.5 sec.
FrequencyInitial
torque
(%U)
50 Hz60%20
Ramp-up
(seconds)
Ramp
down
(seconds)
Input controlled soft start
MCI with by-pass contactor
U
ramp-up
Initial torque
ramp-down
Time
When the control voltage is applied to A1 - A2,
the MCI soft starter will start the motor, according
to the settings of the ramp-up time and initial
torque adjustments. When the control voltage
is switched OFF, the motor will switch off
instantaneously.
By means of the built-in auxiliary contact (23-24)
the by-pass function is easily achieved, see wiring
diagram beside.
Thermal magnetic circuit breaker ............................................ CB
CB
MPM
S
DGT
SSH
16FRCC.PC.026.A4.02
Application Guidelines
Electrical data, connections and wiring
Motor protection
Phase sequence and reverse
rotation protection
CH Compressor models are delivered with a
pre-installed motor protection module inside the
terminal box. This device provides for efficient
and reliable protection against overheating and
overloading as well as phase loss/reversal.
The motor protector comprises a control module
and PTC sensors embedded in the motor
winding. The close contact between thermistors
and windings ensures a very low level of thermal
inertia.
The motor temperature is being constantly
measured by a PTC thermistor loop connected
on S1-S2. If any thermistor exceeds its response
temperature, its resistance increases above the
trip level (4,500 Ω) and the output relay then
trips – i.e. contacts M1-M2 are open. After cooling
to below the response temperature (resistance
< 2,750 Ω), a 5-minute time delay is activated.
Use a phase meter to establish the phase
orders and connect line phases L1, L2 and L3
to terminals T1, T2 and T3, respectively. The
compressor will only operate properly in a single
direction, and the motor is wound so that if the
connections are correct, the rotation will also be
correct.
After this delay has elapsed, the relay is once
again pulled in – i.e. contacts M1-M2 are closed.
The time delay may be cancelled by means
of resetting the mains (L-N -disconnect) for
approximately 5 sec.
When present, the LED on module will lighten as
follows in case of overheat:
PTC overheat
40ms40ms460ms460ms
Appr. 1 second
Delay timer active (after PTC over temp.)
920ms80ms
Appr. 1 second
Should one of these parameters be incorrect,
the relay would lock out (contact M1-M2 open).
When present, the led on the module will show
the following blink code:
In case of phase reverse error:
Voltage imbalance
Compressor model CH290 & CH485 are delivered
with an electronic module which provides
protection against phase reversal and phase
loss at start-up. Apply the recommended wiring
diagrams from section “Suggested wiring
diagram logic”. The circuit should be thoroughly
checked in order to determine the cause of the
phase problem before re-energizing the control
circuit. The phase sequencing and phase loss
monitoring functions are active during a 5-sec
window 1 second after compressor start-up
(power on L1-L2-L3).
Compressor
start
Phase monitoring
Phase sequence module logic
0 1 s 6 s
The operating voltage limits are shown in the
table section “Motor voltage”. The voltage applied
to the motor terminals must lie within these
table limits during both start-up and normal
operations. The maximum allowable voltage
120 ms120 ms120 ms400ms
Appro. 760 ms
In case of phase loss error:
500ms 500ms
Appr. 1second
The lockout may be cancelled by resetting the
power mains (disconnect L-N) for approximately
5 seconds.
imbalance is 2%. Voltage imbalance causes high
amperage over one or several phases, which in
turn leads to overheating and possible motor
damage. Voltage imbalance is given by the
formula:
The scroll compressor application range is
influenced by several parameters which need to
be monitored for a safe and reliable operation.
These parameters and the main
recommendations for good practice and safety
devices are explained hereunder.
When choosing a refrigerant, different aspects
must be taken into consideration:
• Legislation (now and in the future)
• Safety
• Application envelope in relation to expected
running conditions
• Compressor capacity and efficiency
Danfoss Commercial Compressors, along with
the whole refrigeration and air conditioning
industry, shares today’s concern about the
environmental issues that are ozone depletion,
global warming and overall energy consumption.
Usual HCFCs refrigerant fluids such as R22
are known to be implicated in these harmful
phenomena, especially ozone depletion due to
their chlorinated content. These substances are
scheduled to be phased-out from production
• Refrigerant and lubricants
• Motor supply
• Compressor ambient temperature
• Application envelope (evaporating
temperature, condensing temperature, return
gas temperature)
• Compressor manufacturer recommendations
and Guidelines
Additional points could influence the final choice:
• Environmental considerations
• Standardisation of refrigerants and lubricants
• Refrigerant cost
• Refrigerant availability
and use in coming years, in accordance with the
international Montreal Protocol (1984).
As a result, new chlorine-free molecules have
been recently developed and are now ready to
replace former fluids. Among those refrigerants,
the HFC blend R410A is admitted by a great
majority of manufacturers to be the most
promising in terms of environmental impact,
stability and efficiency, and is already seen as the
R22 replacement.
Cooling capacity of liquid (kJ/kg.K) at 25°C1.241.541.84
Cooling capacity of vapor (kJ/kg.K) at 1 atm, 25 °C0.6570.8290. 833
Temperature glide (°C)07.4<0.2
CH compressors are to be used with R410A
refrigerant, with polyolester oil.
• R410A’s superior thermodynamical properties
compared to R22 and R407C refrigerants allow
for today’s massive – and necessary – switch to
high efficiency systems.
• Zero Ozone Depletion Potential (ODP): R410A
does not harm the ozone layer.
• Global warming potential (GWP): R410A shows
a relatively high warming potential. However,
the GWP index denotes direct warming effect,
which is relevant only in case of release to the
atmosphere. A more accurate index is T.E.W.I.,
for Total Equivalent Warming Impact, which
• Because of the higher system efficiency it allows
to achieve, R410A is in this regard the best
refrigerant.
• As a near-azeotropic mixture, refrigerant R410A
behaves like an homogeneous substance,
whereas other zeotropic mixtures such as
R407C and other blends suffer a temperature
glide during phase change that lessens thermal
efficiency and makes them difficult to transfer
from a container to another.
• Reduced refrigerant mass flow, permitted by a
higher heat capacity, induce a lower sound level
of the installation as well as more compact and
lighter systems.
takes into account indirect contributions due to
running energy costs.
18FRCC.PC.026.A4.02
Application Guidelines
Operating conditions
POE oilPolyolester oil (POE) is miscible with HFC's
(while mineral oil is not), but has to be evaluated
regarding lubrication ability in compressors.
POE oil has better thermal stability than
refrigerant mineral oil.
Motor supply
CH scroll compressors can be operated at
nominal voltages as indicated section “Motor
voltage”. Under-voltage and over-voltage
Compressor ambient
temperature
CH compressors can be applied from -35°C to
51°C ambient temperature. The compressors
are designed as 100 % suction gas cooled
High ambient temperature
In case of enclosed fitting and high ambient
temperature it’s recommend to check the
temperature of power wires and conformity
to their insulation specification. In case of safe
tripping by the internal compressor overload
Low ambient temperature
Although the compressor itself can withstand
low ambient temperature, the system may
require specific design features to ensure safe
Application envelope
The operating envelopes for CH scroll
compressors is given in the figure below, where
the condensing and evaporating temperatures
represent the range for steady-state operation.
Under transient conditions, such as start-up and
defrost, the compressor may operate outside
this envelope for short periods. The operating
limits serve to define the envelope within
which reliable operations of the compressor are
guaranteed:
POE is more hygroscopic and also holds moisture
more tight than mineral oil.
It also chemically reacts with water leading to
acid and alcohol formation.
operation is allowed within the indicated voltage
ranges. In case of risk of under-voltage operation,
special attention must be paid to current draw.
without need for additional fan cooling.
Ambient temperature has very little effect on the
compressor performance.
protection the compressor must cool down to
about 60°C before the overload will reset. A high
ambient temperature can strongly delay this
cool-down process.
and reliable operation. See section ‘Specific
application recommendations’.
• Maximum discharge gas temperature: +135°C,
• Due to the risk of liquid flood back the minimum
suction superheat allowed is 5 K
• Maximum superheat of 30 K,
• Minimum and maximum evaporating and
condensing temperatures as per the operating
envelopes.
85
80
75
70
65
60
55
50
45
40
37.8
35
30
26.7
25
20
Condensing temperature (°C)
15
10
5
0
-5
-10
-35-40-45-30-25-20-15-10-5051015202530
-23.31.7 4.412.8-26.1
Evaporating temperature (°C)
SH 10KSH 5K
Map CH290
19FRCC.PC.026.A4.02
Bracket
Application Guidelines
Operating conditions
85
80
75
70
68.3
65
62
60
55
50
45
41.7
40
35
30
25
20
Condensing temperature (°C)
15
10
5
0
-5
-10
-35-40-45-30-25-20-15-10-5051015202530
Evaporating temperature (°C)
SH 30KSH 5KSH 10K
Map CH485
Discharge temperature
protection
The discharge gas temperature must not exceed
135°C.
The discharge gas thermostat accessory kit (code
7750009) includes all components required for
installation as shown below. The thermostat must
be attached to the discharge line within 150 mm
from the compressor discharge port and must be
thermally insulated and tightly fixed on the pipe.
A DGT protection is required if the high and
low pressure switch settings do not protect
the compressor against operations beyond its
specific application envelope. Please refer to
the examples below, which illustrate where DGT
protection is required (Ex.1) and where it is not
(Ex.2). A discharge gas temperature protection
device must be installed on all heat pumps. In
reversible air-to-air and air-to-water heat pumps
70
65
Example 1 (R410A)
LP switch setting:
LP1 = 3.3 bar (g) (-15.5°C)
HP switch setting:
HP1 = 38 bar (g) (62°C)
Risk of operation beyond the application envelope.
DGT protection required.
Example 2 (R410A)
LP switch setting:
LP2 = 4.6 bar (g) (-10.5°C)
HP switch setting:
HP2 = 31 bar (g) (52°C)
No risk of operation beyond the
application envelope.
No DGT protection required.
60
55
50
45
40
35
Cond. temp. (°C)
30
25
20
15
10
-30-25-20-15
Thermostat
Discharge line
Insulation
the discharge temperature must be monitored
during development test by the equipment
manufacturer. The DGT should be set to open
at a discharge gas temperature of 135°C. The
compressor must not be allowed to cycle on the
discharge gas thermostat. Continuous operations
beyond the compressor’s operating range will
cause serious damage to the compressor!
Example 1
DGT - limit
LP1
LP2
-10
Evap. temp. (°C)
Example 2
Map example R410A
-505101520
HP1
HP2
20FRCC.PC.026.A4.02
T
~
~
Application Guidelines
High and low pressure
protection
Operating conditions
High pressure
Low pressure
A high-pressure (HP) safety switch is required to
shut down the compressor should the discharge
pressure exceed the values shown in the table
section “System pressure test”. The high-pressure
switch can be set to lower values depending on
the application and ambient conditions. The HP
A low-pressure (LP) safety switch must be used.
Deep vacuum operations of a scroll compressor
can cause internal electrical arcing and scroll
instability. Danfoss CH Scroll compressors exhibit
high volumetric efficiency and may draw very
low vacuum levels, which could induce such
a problem. The minimum low-pressure safety
switch (loss-of-charge safety switch) setting is
Pressure settingsR410A
Working pressure range high side bar (g)16.2 - 41.6
Working pressure range low side bar (g)2.15 - 10.7
Maximum high pressure safety switch setting bar (g)46.1
Minimum low pressure safety switch setting * bar (g)1.5
Minimum low pressure pump-down switch setting ** bar (g)2.15
* LP safety switch shall never be bypassed and shall have no time delay.
** Recommended pump-down switch settings: 1.5 bar below nominal evap. pressure with minimum of 2.15 bar(g)
switch must either be placed in a lockout circuit
or consist of a manual reset device to prevent
cycling around the high-pressure limit. If a
discharge valve is used, the HP switch must be
connected to the service valve gauge port, which
must not be isolated.
given in the following table. For systems without
pump-down, the LP safety switch must either be
a manual lockout device or an automatic switch
wired into an electrical lockout circuit. The LP
switch tolerance must not allow for vacuum
operations of the compressor. LP switch settings
for pump-down cycles with automatic reset are
also listed in the table below.
Note that these two different low pressure
switches also require different settings. The
low pressure pump down switch setting must
always be within the operating envelope, for
example 2.15 bar for R410A. The compressor
can be operated full time under such condition.
Cycle rate limitDanfoss recommends a restart delay timer to
limit compressor cycling. The timer prevents
reverse compressor rotation, which may occur
during brief power interruptions.
The system must be designed in a way that
guarantees a minimum compressor running
time of 2 minutes so as to provide for sufficient
motor cooling after start-up along with proper oil
return. Note that the oil return may vary since it
depends upon system design. There must be no
more than 12 starts per hour, a number higher
than 12 reduces the service life of the motor-
The minimum low pressure safety switch setting
may be outside the normal operating envelope
and should only be reached in exceptional
(emergency) situations, for example 1.5 bar for
R410A.
compressor unit. A three-minute (180- sec) time
out is recommended.
KA
A1
H
TT
A2
TH
KA
A2 A3A1
180 s
Please contact Danfoss Technical Support for any
deviation from these guidelines.
21FRCC.PC.026.A4.02
Application Guidelines
System design recommendations
General
Essential piping design
recommendations
Successful application of scroll compressors
is dependent on careful selection of the
compressor for the application. If the compressor
is not correct for the system, it will operate
The working pressure in systems with R410A is
about 60% higher than in systems with R22 or
R407C. Consequently, all system components and
piping must be designed for this higher pressure
level.
Proper piping practices should be employed to
ensure adequate oil return, even under minimum
load conditions with special consideration given
to the size and slope of the tubing coming
from the evaporator. Tubing returns from the
evaporator should be designed so as not to trap
oil and to prevent oil and refrigerant migration
back to the compressor during off-cycles.
In systems with R410A, the refrigerant mass
flow will be lower compared to R22/R407C
systems. To maintain acceptable pressure
drops and acceptable minimum gas velocities,
the refrigerant piping must be reduced in size
beyond the limits given in this manual. Poor
performance, reduced reliability, or both may
result.
compared to R22 / R407C systems. Take care not
to create too high pressure drops since in R410A
systems the negative impact of high pressure
drops on the system efficiency is stronger than in
R22/R407C systems.
Piping should be designed with adequate threedimensional flexibility. It should not be in contact
with the surrounding structure, unless a proper
tubing mount has been installed. This protection
proves necessary to avoid excess vibration, which
can ultimately result in connection or tube failure
due to fatigue or wear from abrasion. Aside from
tubing and connection damage, excess vibration
may be transmitted to the surrounding structure
and generate an unacceptable noise level within
that structure as well. For more information on
noise and vibration, see the section on: “Sound
and vibration management”.
Suction lines
Discharge lines
If the evaporator lies above the compressor, as
is often the case in split or remote condenser
systems, the addition of a pump-down cycle
is strongly recommended. If a pump-down
cycle were to be omitted, the suction line must
have a loop at the evaporator outlet to prevent
refrigerant from draining into the compressor
during off-cycles.
If the evaporator were situated below the
compressor, the suction riser must be trapped so
as to prevent liquid refrigerant from collecting at
the outlet of the evaporator while the system is
idle, which would mislead the expansion valve’s
sensor (thermal bulb) at start-up.
When the condenser is mounted at a higher
position than the compressor, a suitably sized
“U”-shaped trap close to the compressor is
necessary to prevent oil leaving the compressor
from draining back to the discharge side of the
compressor during off cycle. The upper loop also
helps avoid condensed liquid refrigerant from
draining back to the compressor when stopped.
max. 4 m
max. 4 m
Upper loop
U Trap
U-trap
0.5% slope
4 m/s or more
U-trap, as short as possible
8 to 12 m/s
0.5% slope
4m/s or more
U trap, as short as possible
HP
To condenser
HP
LP
Evaporator
Condenser
22FRCC.PC.026.A4.02
LP
3D exibility
Application Guidelines
System design recommendations
Heat exchangers
To obtain optimum efficiency of the complete
refrigerant system, optimised R410A heat
exchangers must be used. R410A refrigerant has
good heat transfer properties: it is worthwhile
designing specific heat exchangers to gain in size
and efficiency.
An evaporator with optimised R410A distributor
and circuit will give correct superheat at outlet
and optimal use of the exchange surface. This is
critical for plate evaporators that have generally a
shorter circuit and a lower volume than shell and
tubes and air cooled coils.
For all evaporator types a special care is required
for superheat control leaving the evaporator and
oil return.
Refrigerant charge limitDanfoss CH compressors can tolerate liquid
refrigerant up to a certain extend without major
problems. However, excessive liquid refrigerant in
the compressor is always unfavorable for service
life. Besides, the installation cooling capacity may
be reduced because of the evaporation taking
place in the compressor and/or the suction line
instead of the evaporator. System design must be
such that the amount of liquid refrigerant in the
compressor is limited. In this respect, follow the
A sub-cooler circuit in the condenser that creates
high sub cooling will increase efficiency at high
condensing pressure. In R410A systems the
positive effect of sub cooling on system efficiency
will be significantly larger than in R22/R407C
systems.
Furthermore, for good operation of the
expansion device and to maintain good
efficiency in the evaporator it is important
to have an appropriate sub cooling. Without
adequate sub cooling, flash gas will be formed at
the expansion device resulting in a high degree
of vapour at the expansion device inlet leading to
low efficiency.
guidelines given in the section: “Essential piping
design recommendations” in priority.
Use the tables below to quickly evaluate the
required compressor protection in relation with
the system charge and the application.
Model
CH29013.5
CH48517
Refrigerant charge limit
(kg)
Cooling only systems,
Packaged units
Cooling only systems
with remote condenser
and split system units
Reversible heat pump system
BELOW charge limitABOVE charge limit
Refrigerant migration and flood back test
No test or additional safeties required
Refrigerant migration and flood back test
REC
Sump heater
REC
Specific tests for repetitive flood back
REQ
Sump heater
REQ
Defrost test For more details, refer to section ”Reversible heat pump system“
REQ
RecommendedRequiredNo test or additional safeties required
REC
Note: for special conditions such as low ambient temperature, low refrigerant load or brazed plate heat exchangers please refer to
corresponding sections.
REQ
REQ
Sump heater
REQ
Refrigerant migration and flood back test
REQ
Sump heater
REQ
Liquid receiver (in association with LLSV and
REC
pump down)
More detailed information can be found in the paragraphs hereafter.
Please contact Danfoss Technical Support for any deviation from these guidelines.
23FRCC.PC.026.A4.02
Application Guidelines
System design recommendations
Off-cycle migration
Sump heater
Off -cycle refrigerant migration is likely to occur
when the compressor is located at the coldest
part of the installation, when the system uses
a bleed-type expansion device, or if liquid is
allowed to migrate from the evaporator into
the compressor sump by gravity. If too much
liquid refrigerant accumulates in the sump it
will saturate the oil and lead to a flooded start:
when the compressor starts running again, the
refrigerant evaporates abruptly under the sudden
decrease of the bottom shell pressure, causing
the oil to foam. In extreme situations, this might
result in liquid slugging (liquid entering the scroll
elements), which must be avoided as it causes
irreversible damage to the compressor.
Danfoss CH scroll compressors can tolerate
occasional flooded starts as long as the total
system charge does not exceed the maximum
compressor refrigerant charge. A suitable test
to evaluate the risk of off –cycle migration is the
following:
The surface sump heaters are designed to protect
the compressor against off-cycle migration of
refrigerant.
When the compressor is idle, the oil temperature
in the sump of the compressor must be
maintained at no lower than 10 K above the
saturation temperature of the refrigerant on the
low-pressure side. This requirement ensures that
the liquid refrigerant is not accumulating in the
sump. A sump heater is only effective if capable
of sustaining this level of temperature difference.
Tests must be conducted to ensure that the
appropriate oil temperature is maintained under
all ambient conditions (temperature and wind).
Note that below -5°C ambient temperature and a
wind speed of above 5m/second, we recommend
that the heaters be thermally insulated in order
to limit the surrounding energy losses.
Since the total system charge may be undefined,
a sump heater is recommended on all standalone compressors and split systems. In addition,
any system containing a refrigerant charge in
excess of the maximum recommended system
charge for compressors requires a sump heater.
A sump heater is also required on all reversible
cycle applications.
• Stabilize the non-running system at 5°C
ambient temperature,
• Raise the ambient temperature to 20°C and
keep it for 10 minutes,
• Start the compressor and monitor sump
temperature, sight glass indication and sound
level.
The presence of liquid in the crankcase can be
easily detected by checking the sump level
through the oil sight glass. Foam in the oil sump
indicates a flooded start.
A noisy start, oil loss from the sump and sump
cool down are indications for migration.
Depending on the amount of migration graduate
measures shall be taken:
• Sump heater
• Liquid line solenoid valve
• Pump down cycle
on
off
Compressor 1
Compressor 2
Compressor 3
on
off
on
off
The heater must be energized whenever the
compressor is off to avoid liquid refrigerant
entering the compressor.
Provide separate electrical supply for the heaters
so that they remain energized even when
the machine is out of service (e.g. seasonal
shutdown).
Surface sump heater accessories are available
from Danfoss (see section “Accessories”).
24FRCC.PC.026.A4.02
At initial start-up or after power shortage, it is
recommended to energize surface sump heater
to remove refrigerant 6 hours in advance. A
quicker start-up is possible by “jogging” the
compressor to evacuate refrigerant in the
compressor.
Application Guidelines
System design recommendations
Liquid line solenoid valve
(LLSV)
Pump-down cyclePump-down cycle represents one of the most
A LLSV may be used to isolate the liquid charge
on the condenser side, thereby preventing
against charge transfer or excessive migration to
the compressor during off-cycles. The quantity of
effective ways to protect against the off –cycle
migration of liquid refrigerant. Once the system
has reached its set point and is about to shut
off, the LLSV on the condenser outlet closes.
The compressor then pumps the majority of
the refrigerant charge into the condenser and
receiver before the system stops on the low
pressure pump-down switch. This step reduces
the amount of charge on the low side in order to
prevent off -cycle migration. The recommended
low-pressure pump-down switch setting is 1.5
bar below the nominal evaporating pressure.
It shall not be set lower than 2.15 bar(g). For
suggested wiring diagrams, please see section
«Suggested wiring diagrams logic».
Tests for pump down cycle approval:
• As the pump-down switch setting is inside the
application envelope, tests should be carried out
to check unexpected cut-out during transient
conditions (ie. defrost – cold starting). When
unwanted cut-outs occur, the low pressure
pump-down switch can be delayed. In this case
refrigerant on the low-pressure side of the system
can be further reduced by using a pump-down
cycle in association with the LLSV.
a low pressure safety switch without any delay
timer is mandatory. While the thermostat is off,
the number of pressure switch resets should be
limited to avoid short cycling of the compressor.
Use dedicated wiring and an additional relay
which allows for one shot pump-down.
The pump-down allows to store all the refrigerant
in the high pressure side circuit. On unitary
or close-coupled systems, where the system
refrigerant charge is expected to be both correct
and definable the entire system charge may be
stored in the condenser during pump-down if
all components have been properly sized. Other
application needs a liquid receiver to store the
refrigerant.
Receiver dimensioning requires special attention.
The receiver shall be large enough to contain
part of the system refrigerant charge but it shall
not be dimensioned too large. A large receiver
easily leads to refrigerant overcharging during
maintenance operation.
25FRCC.PC.026.A4.02
Application Guidelines
System design recommendations
Liquid flood back
During normal operation, refrigerant enters the
compressor as a superheated vapour. Liquid
flood back occurs when a part of the refrigerant
entering the compressor is still in liquid state.
Danfoss CH scroll compressors can tolerate
occasional liquid flood back. However system
design must be such that repeated and excessive
flood back is not possible.
Liquid flood back test - Repetitive liquid
flood back testing must be carried out under
expansion valve threshold operating conditions:
a high pressure ratio and minimum evaporator
load, along with the measurement of suction
superheat, oil sump temperature and discharge
gas temperature.
During operations, liquid flood back may be
detected by measuring either the oil sump
temperature or the discharge gas temperature.
If at any time during operations, the oil sump
temperature drops to within 10K or less above
Suction accumulator: a suction accumulator
offers protection against refrigerant flood back
at start-up, during operations or defrosting by
trapping the liquid refrigerant upstream from
the compressor. The suction accumulator also
protects against off -cycle migration by providing
additional internal free volume to the low side of
the system.
A suction accumulator must be carefully
dimensioned, taking into account the refrigerant
A continuous liquid flood back will cause oil
dilution and, in extreme situations lead to lack
of lubrication and high rate of oil leaving the
compressor.
the saturated suction temperature, or should
the discharge gas temperature be less than 35K
above the saturated discharge temperature, this
indicates liquid flood back.
Continuous liquid flood back can occur with
a wrong dimensioning, a wrong setting or
malfunction of the expansion device or in case
of evaporator fan failure or blocked air filters.
A suction accumulator providing additional
protection as explained hereunder can be used
to solve light continuous liquid flood back.
charge as well as the gas velocity in the suction
line. The accumulator should not be sized for less
than 50 % of the total system charge. Tests must
be conducted to determine the actual refrigerant
holding capacity needed for the application.
Depending on the operating conditions it may
happen that the recommended connections of
the accumulator are one size smaller than the
suction line.
26FRCC.PC.026.A4.02
Application Guidelines
Low ambient application
Specific application recommendations
Low ambient start-up
Low ambient operations
Under cold ambient conditions (<0°C), upon
start-up the pressure in the condenser may be so
low that a sufficient pressure differential across
the expansion device cannot be developed to
properly feed the evaporator.
As a result, the compressor may go into a deep
vacuum, which can lead to compressor failure
due to internal arcing and instability in the
scroll wraps. Under no circumstances should
the compressor be allowed to operate under
vacuum. The low-pressure control must be set in
accordance with the table section “Low pressure”
in order to prevent this from happening. Early
The Danfoss CH scroll compressor requires a
minimum pressure differential of 6 to 7 bar
between the suction and discharge pressures
to force the orbiting scroll down against the
oil film on the thrust bearing. Anything less
than this differential and the orbiting scroll
can lift up, causing a metal-to-metal contact.
It is therefore necessary to maintain sufficient
discharge pressure in order to ensure this
pressure differential. Care should be taken during
low ambient operations when heat removal
from air-cooled condensers is greatest and
head pressure control may be required for low
ambient temperature applications. Operation
under low pressure differential may be observed
by a significant increase in the sound power level
generated by the compressor.
It is recommended that the unit be tested and
monitored at minimum load and low ambient
conditions as well. The following considerations
should be taken into account to ensure proper
system operating characteristics.
Expansion device: The expansion device
should be sized to ensure proper control of the
refrigerant flow into the evaporator. An oversized
valve may result in erratic control. This can lead
to liquid refrigerant entering the compressor
if the expansion valve does not provide stable
refrigerant super-heat control under varying
loads. The superheat setting of the expansion
device should be sufficient to ensure proper
superheat levels during low loading periods. A
minimum of 5 K stable superheat is required.
feeding of the evaporator and management of
the discharge pressure could help to attenuate
these effects.
Low pressure differentials can also cause
the expansion device to «hunt» erratically,
which might cause surging conditions within
the evaporator, with liquid spillover into the
compressor. This effect is most pronounced
during low load conditions, which frequently
occur during low ambient conditions.
Head pressure control under low ambient
conditions: Several possible solutions are
available to prevent the risk of compressor to
vacuum and low pressure differential between
the suction and discharge pressures.
In air-cooled machines, cycling the fans with
a head pressure controller will ensure that the
fans remain off until the condensing pressure
has reached a satisfactory level. Variable speed
fans can also be used to control the condensing
pressure. In water-cooled units, the same can be
performed using a water regulator valve that is
also operated by head pressure, thereby ensuring
that the water valve does not open until the
condensing pressure reaches a satisfactory level.
The minimum condensing pressure must be
set at the minimum saturated condensing
temperature shown in the application envelopes.
Under very low ambient conditions, in which
testing has revealed that the above procedures
might not ensure satisfactory condensing and
suction pressures, the use of a head pressure
control valve is recommended. Note: This
solution requires extra refrigerant charge, which
can introduce other problems. A non-return
valve in the discharge line is recommended and
special care should be taken when designing the
discharge line.
For further information, please contact Danfoss.
27FRCC.PC.026.A4.02
Application Guidelines
Specific application recommendations
Sump heaters
Low load operation
Brazed plate heat
exchangers
Sump heaters are strongly recommended on
all systems where the compressor is exposed to
low ambient temperatures, especially split and
remote condenser installations. The sump heater
The compressors should be run for a
minimum period in order to ensure that the
oil has sufficient time to properly return to the
A brazed plate heat exchanger needs very little
internal volume to satisfy the set of heat transfer
requirements. Consequently, the heat exchanger
offers very little internal volume for the
compressor to draw vapour from on the suction
side. The compressor can then quickly enter into
a vacuum condition. It is therefore important
that the expansion device be sized correctly
and that a sufficient pressure differential across
the expansion device be available to ensure
adequate refrigerant feed into the evaporator.
This aspect is of special concern when operating
the unit under low ambient and load conditions.
For further information on these conditions,
please refer to the previous sections.
Due to the small volume of the brazed plate heat
exchanger, no pump-down cycle is normally
will minimize refrigerant migration caused by
the large temperature gradient between the
compressor and the remainder of the system,
please refer to section “Accessories”.
compressor sumps and that the motor has
sufficient time to cool under conditions of lowest
refrigerant mass flows.
required. The suction line running from the heat
exchanger to the compressor must be trapped to
avoid refrigerant migration to the compressor.
When using a brazed plate condenser heat
exchanger, a sufficient free volume for the
discharge gas to accumulate is required in order
to avoid excess pressure build-up. At least 1
meter of discharge line is necessary to generate
this volume.
To help reduce the gas volume immediately after
start-up even further, the supply of cooling water
to the heat exchanger may be opened before the
compressor starts up so as to remove superheat
and condense the incoming discharge gas more
quickly.
Electronic expansion
valve
Reversible heat pump
systems
The use of an electronic expansion valve requires
a specific compressor start / stop control.
Specific compressor start sequence control has
to be set when an electronic expansion valve
(EXV) is used. The sequence must be adjusted
according to the EXV step motor speed to allow
time for the EXV to open before the compressor
starts to avoid running under vacuum conditions.
The EXV should be closed at compressor stop
not to let refrigerant in liquid phase entering the
Transients are likely to occur in reversible heat
pump systems, i.e. a changeover cycle from
cooling to heating, defrost or low-load short
cycles. These transient modes of operation
may lead to liquid refrigerant carry-over (or
flood back) or excessively wet refrigerant return
conditions. As such, reversible cycle applications
require specific precautions for ensuring a long
compressor life and satisfactory operating
characteristics. Regardless of the refrigerant
compressor. Ensure that the EXV closes when the
supply voltage to the controller is interrupted (ie
power cut off) by the use of a battery back-up.
EXV Opened
Closed
Compressor On
Off
charge in the system, specific tests for repetitive
flood back are required to confirm whether or not
a suction accumulator needs to be installed.
The following considerations cover the most
important issues when dealing with common
applications. Each application design however
should be thoroughly tested to ensure
acceptable operating characteristics.
28FRCC.PC.026.A4.02
Application Guidelines
Specific application recommendations
Sump heatersSump heaters are mandatory on reversible
cycle applications given the high probability of
liquid migration back to the compressor sump
Discharge temperature
thermostat
Discharge line, reversing
valve, solenoid valves
Heat pumps frequently utilize high condensing
temperatures in order to achieve a sufficient
temperature rise in the medium being heated.
At the same time, they often require low
evaporating pressures to obtain sufficient
temperature differentials between the evaporator
and the outside temperature. This situation may
result in high discharge temperature; as such,
it is mandatory that a discharge gas thermostat
be installed on the discharge line to protect
The Danfoss CH scroll compressor is a high
volumetric machine and, as such, can rapidly
build up pressure in the discharge line if gas
in the line becomes obstructed even for a very
short period of time which situation may occur
with slow-acting reversing valves in heat pumps.
Discharge pressures exceeding the operating
envelope may result in nuisance high-pressure
switch cutouts and place excess strain on both
the bearings and motor.
To prevent such occurrences, it is important that
a 1-meter minimum discharge line length be
allowed between the compressor discharge port
during off -cycles due to the outdoor location of
most units and operations during low ambient
conditions.
the compressor from excessive temperatures.
Operating the compressor at too high discharge
temperatures can result in mechanical damage
to the compressor as well as thermal degradation
of the compressor lubricating oil and a lack
of sufficient lubrication. The discharge gas
thermostat should be set to shut down the
compressor in the event discharge gas rises
above 135°C.
and the reversing valve or any other restriction.
This gives sufficient free volume for the discharge
gas to collect and to reduce the pressure peak
during the time it takes for the valve to change
position. At the same time, it is important that
the selection and sizing of the reversing or 4-way
valve ensure that the valve switches quickly
enough to prevent against too high discharge
pressure and nuisance high-pressure cutouts.
Check with the valve manufacturer for optimal
sizing and recommended mounting positions.
29FRCC.PC.026.A4.02
Application Guidelines
Specific application recommendations
Defrost and reverse cycle
Suction line accumulator
In applications with heat recovery or condenser
partialisation, servo piloted solenoid valve have
to be properly sized or associated with a second
small valve in parallel, in order to avoid quick
The Danfoss CH scroll compressor have the
ability to withstand a certain amount of liquid
refrigerant dynamic slug.
When compressors are installed in parallel,
in order to limit liquid amount handled per
compressor when beginning and ending defrost,
it is recommended to avoid running part load
(keep all compressors running or keep them
stopped when moving 4-way valves).
For further details, please refer to Parallel
application guidelines
The use of a suction line accumulator is strongly
recommended in reversible-cycle applications.
This because of the possibility of a substantial
quantity of liquid refrigerant remaining in the
evaporator, which acts as a condenser during the
heating cycle.
This liquid refrigerant can then return to the
compressor, either flooding the sump with
refrigerant or as a dynamic liquid slug when
discharge pressure drops when opening. This
phenomenon could lead to hammering effects
and create constraints on the non-return valve
integrated in discharge fitting.
EXV can also be opened when compressors are
stopped and before 4 way valve is moving in
order to decrease pressure difference. Opening
degree and time have to be set in order to keep
a minimum pressure difference for 4 way valve
moving. Each application design however should
be thoroughly tested to ensure acceptable
operating characteristics.
the cycle switches back to a defrost cycle or to
normal cooling operations.
Sustained and repeated liquid slugging and
flood back can seriously impair the oil’s ability
to lubricate the compressor bearings. This
situation can be observed in wet climates where
it is necessary to frequently defrost the outdoor
coil in an air source heat pump. In such cases a
suction accumulator becomes mandatory.
Water utilizing systems
Apart from residual moisture in the system
after commissioning, water could also enter the
refrigeration circuit during operation. Water in
the system shall always be avoided. Not only
because it can shortly lead to electrical failure,
sludge in sump and corrosion but in particular
because it can cause serious safety risks.
Common causes for water leaks are corrosion and
freezing.
Corrosion: Materials in the system shall be
compliant with water and protected against
corrosion.
Freezing: When water freezes into ice its volume
expands which can damage heat exchanger
walls and cause leaks. During off periods water
inside heat exchangers could start freezing when
ambient temperature is lower than 0°C. During
on periods ice banking could occur when the
circuit is running continuously at too low load.
Both situations should be avoided by connecting
a pressure and thermostat switch in the safety
line.
30FRCC.PC.026.A4.02
Application Guidelines
Sound and vibration management
Starting sound level
Running sound level
Stopping sound level
During start-up transients it is natural for the
compressor sound level to be slightly higher
than during normal running. The CH scroll
compressors exhibit very little increased start-up
transient sound. If a compressor is miswired,
compressor rotation is characterized by an
objectionable sound. To correct reverse rotation,
disconnect power and switch any two of the
three power leads at the unit contactor. Never
switch leads at the compressor terminals.
the compressor will run in reverse. Reverse
Compressor acoustic hoods have been
developed to meet specific extra-low noise
incorporate sound proofing materials and offer
excellent high and low frequency attenuation.
requirements. The covers and bottom insulations
50 Hz
Model
CH290826120Z0 022120Z0 353
CH485894120Z0 022120Z0353
Sound power and attenuation are given at ARI conditions, measured in free space
Attenuation given with acoustic hood only
Bottom hood is provided in surface sump heater accessories. Additional attenuation is 2 to 4 dBA. Materials are UL approved and
RoHS compliant.
Sound power dB(A)
CH compressors are equipped with a discharge
valve which closes at compressor shut down
and thus prevents the compressor from running
backwards. This reduces the stopping sound to a
Attenuation
dBA
When the pressure difference or gas flow at shut
down should be very low, this can delay the
discharge valve from closing and lead to a longer
noise duration.
Acoustic hood code
number
Bottom hood code
number
metallic click caused by the closing valve.
Sound generation in a
refrigeration or air
conditioning system
Typical sound and vibration in refrigeration and
air conditioning systems encountered by design
and service engineers may be broken down into
the following three source categories.
Sound radiation: this generally takes an airborne
path.
Mechanical vibrations: these generally extend
along the parts of the unit and structure.
Gas pulsation: this tends to travel through the
cooling medium, i.e. the refrigerant.
The following sections focus on the causes and
methods of mitigation for each of the above
sources.
31FRCC.PC.026.A4.02
Application Guidelines
Sound and vibration management
Compressor sound radiationFor sound radiating from the compressor, the
emission path is airborne and the sound waves
are travelling directly from the machine in all
directions.
The CH scroll compressors are designed to be
quiet and the frequency of the sound generated
is pushed into the higher ranges, which not only
are easier to reduce but also do not generate the
penetrating power of lower frequency sound.
Use of sound-insulation materials on the inside of
unit panels is an effective means of substantially
reducing the sound being transmitted to the
outside. Ensure that no components capable
of transmitting sound/vibration within the unit
come into direct contact with any non-insulated
parts on the walls of the unit.
Mechanical vibrations
Vibration isolation constitutes the primary
method for controlling structural vibration.
Danfoss CH scroll compressors are designed to
produce minimal vibration during operations.
Once the supplied rubber grommets have been
properly mounted, vibrations transmitted from
the compressor base plate to the unit are held
to a strict minimum. In addition, it is extremely
important that the frame supporting the
mounted compressor be of sufficient mass and
stiffness to help dampen any residual vibration
potentially transmitted to the. For further
information on mounting requirements, please
refer to the section on mounting assembly.
Because of the unique Danfoss design of a
full-suction gas-cooled motor, compressor
body insulation across its entire operating
range is possible. Acoustic hoods are available
from Danfoss as accessories. They have been
developed to meet specific extra low noise
requirements. They incorporate sound proofing
materials and offer excellent high and low
frequency alternative.
These hoods are quick and easy to install and do
not increase the overall size of the compressors
to a great extend.
Refer to section “Running sound level” for sound
attenuation and code numbers.
Note: For parallel assemblies see specific
recommendations in Danfoss parallel application
guidelines (Rigid mounting).
The tubing should be designed so as to both
reduce the transmission of vibrations to other
structures and withstand vibration without
incurring any damage. Tubing should also be
designed for three-dimensional flexibility. For
more information on piping design, please see
the section entitled “Essential piping design
considerations”.
Gas pulsation
The Danfoss CH scroll compressors have been
designed and tested to ensure that gas pulsation
has been optimised for the most commonly
encountered air conditioning pressure ratio. On
heat pump installations and other installations
where the pressure ratio lies beyond the
typical range, testing should be conducted
under all expected conditions and operating
configurations to ensure that minimum gas
pulsation is present. If an unacceptable level
is identified, a discharge muffler with the
appropriate resonant volume and mass should
be installed. This information can be obtained
from the component manufacturer.
32FRCC.PC.026.A4.02
Application Guidelines
Installation
Compressor handling and
storage
Each CH compressor is shipped with printed
Instructions for installation. These instructions
can also be downloaded from our web site:
Each Danfoss CH scroll compressor is equipped
with two lift rings on the top shell. Always use
both these rings when lifting the compressor.
Use lifting equipment rated and certified for
the weight of the compressor. A spreader
bar rated for the weight of the compressor is
highly recommended to ensure a better load
distribution. The use of lifting hooks closed
with a clasp and certified to lift the weight of
the compressor is also highly recommended.
Always respect the appropriate rules concerning
lifting objects of the type and weight of these
compressors.
Maintain the compressor in an upright position
during all handling man oeuvres (maximum of
15° from vertical).
Never use only one lifting lug to lift the
compressor. The compressor is too heavy for the
single lug to handle, and the risk is run that the
lug could separate from the compressor with
extensive damage and possible personal injury
as a result.
www.danfoss.com or directly from: http://www.
danfoss.com/China/
Store the compressor not exposed to rain,
corrosive or flammable atmosphere and between
-35°C and 51°C when charged with R410A
refrigerant and between -35°C and 70°C when
charged with nitrogen.
When the compressor is mounted as part
of an installation, never use the lift rings on the
compressor to lift the installation. The risk is run
that the lugs could separate from the compressor
or that the compressor could separate from the
base frame with extensive damage and possible
personal injury as a result.
Never apply force to the terminal box with the
intention of moving the compressor, as the
force placed upon the terminal box can cause
extensive damage to both the box and the
components contained inside.
HEAVY
do not lift
manually
33FRCC.PC.026.A4.02
Application Guidelines
Installation
Compressor mounting
Mounting
Maximum inclination from the vertical plane while operating must not exceed 3 degrees.
Compressors CH290 & 485 dedicated for
parallel (versions AA and AB) mounting come
delivered with rigid mounting spacers for parallel
mounting.
CH290 used in single applications, are delivered
with flexible grommets. The grommets must
be compressed until contact between the
Manifoldable compressor
with rigid spacers
flat washer and the steel mounting sleeve is
established. The grommets attenuate to a great
extent the transmission of compressor vibrations
to the base frame.
The required bolt size for the CH290 & 485
compressors is HM8-55. This bolt must be
tightened to a torque of 21 Nm.
Single compressor
with rubber grommets
Compressor holding
charge
HM 8 bolt
Lock washer
Nut
Flat washer
29.5 mm
Rigid spacer
Nut
Each compressor is shipped with a nominal dry
nitrogen holding charge between 0.3 and 0.7 bar
and is sealed with elastomer plugs.
Before the suction and discharge plugs are
removed, the nitrogen holding charge must be
released via the suction schrader valve to avoid
an oil mist blowout. Remove the suction plug
HM 8 bolt
Lock washer
Flat washer
Steel mounting sleeve
Rubber grommet
Nut
Compressor
base plate
27.5 mm
first and the discharge plug afterwards. The plugs
shall be removed only just before connecting the
compressor to the installation in order to avoid
moisture from entering the compressor. When
the plugs are removed, it is essential to keep the
compressor in an upright position so as to avoid
oil spillage.
34FRCC.PC.026.A4.02
Application Guidelines
Installation
System cleanliness
The refrigerant compression system, regardless
of the type of compressor used, will only provide
high efficiency and good reliability, along with a
long operating life, if the system contains solely
the refrigerant and oil it was designed for. Any
other substances within the system will not
improve performance and, in most cases, will be
highly detrimental to system operations.
The presence of non-condensable substances
and system contaminants such as metal
shavings, solder and flux, have a negative
impact on compressor service life. Many of these
contaminants are small enough to pass through
a mesh screen and can cause considerable
damage within a bearing assembly. The use of
highly hygroscopic polyol ester oil in R410A
compressors requires that the oil be exposed
to the atmosphere as little as possible. System
TubingOnly use clean and dehydrated refrigeration
grade copper tubing. Tube-cutting must be
carried out so as not to deform the tubing
roundness and to ensure that no foreign debris
remains within the tubing. Only refrigerant grade
fittings should be used and these must be of
contamination is one of main factors affecting
equipment reliability and compressor service
life. It is important therefore to take system
cleanliness into account when assembling a
refrigeration system.
During the manufacturing process, circuit
contamination may be caused by:
• Brazing and welding oxides,
• Filings and particles from the removal of burrs
in pipe-work,
• Brazing flux,
• Moisture and air.
Consequently, when building equipment
and assemblies, the precautions listed in the
following paragraphs must be taken.
both a design and size to allow for a minimum
pressure drop through the completed assembly.
Follow the brazing instructions on next pages.
Never drill holes into parts of the pipe-work
where fi lings and particles can not be removed.
Brazing and soldering
Do not bend the compressor discharge or suction
lines or force system piping into the compressor
connections, because this will increase
stresses that are a potential cause of failure.
Recommended brazing procedures and material,
Copper to copper
connections
When brazing copper-to-copper connections,
the use of copper/phosphorus brazing alloy
containing 5% silver or more with a melting
Dissimilar metals
connection
When manipulating dissimilar metals such as
copper and brass or steel, the use of silver solder
(5% or more) and anti-oxidant flux is necessary.
Compressor connectionWhen brazing the compressor fittings, do not
overheat the compressor shell, which could
severely damage certain internal components
due to excessive heating. Use of a heat shield
and/or a heat-absorbent compound is highly
recommended. Due to the relatively sizable
tubing and fitting diameters a double-tipped
torch using acetylene is recommended for
brazing operation on CH scroll compressors.
are described section “Compressor connection”.
These operations must be performed by a
qualified personnel in compliance with all
pertinent practices and safety procedures.
temperature of below 800°C is recommended. No
flux is required during brazing.
Please contact Danrfoss Technical support for any
deviation from this guidelines.
heat shield
A
C
B
35FRCC.PC.026.A4.02
Application Guidelines
Installation
For brazing the suction and discharge
connections, the following procedure is advised:
.Make sure that no electrical wiring is connected
to the compressor.
.Protect the terminal box and compressor
painted surfaces from torch heat damage (see
diagram).
.Remove the Teflon gaskets when brazing
rotolock connectors with solder sleeves.
.Use only clean refrigeration-grade copper
tubing and clean all connections.
.Use brazing material with a minimum of 5%
silver content.
.Purge nitrogen or CO
through the compressor
2
in order to prevent against oxidation and
flammable conditions. The compressor should
not be exposed to the open air for extended
periods.
.Use of a double-tipped torch is recommended.
.Apply heat evenly to area A until the brazing
temperature is reached. Move the torch to
area B and apply heat evenly until the brazing
temperature has been reached there as well,
and then begin adding the brazing material.
Move the torch evenly around the joint, in
applying only enough brazing material to flow
the full circumference of the joint.
.Move the torch to area C only long enough to
draw the brazing material into the joint, but not
into the compressor.
.Remove all remaining flux once the joint has
been soldered with a wire brush or a wet cloth.
Remaining flux would cause corrosion of the
tubing.
In addition, for discharge connections equipped
with a non return valve integrated in discharge
fitting the direction of the torch has to be as
described on the picture, and maximum brazing
time should be less than 2 minutes to avoid NRVI
damages.
Ensure that no flux is allowed to enter into the
tubing or compressor. Flux is acidic and can cause
substantial damage to the internal parts of the
system and compressor.
The polyolester oil used in CH compressors
is highly hygroscopic and will rapidly absorb
moisture from the air. The compressor must
therefore not be left open to the atmosphere
for a long period of time. The compressor fitting
plugs shall be removed just before brazing the
compressor. The compressor should always be
the last component brazed into the system
Before eventual unbrazing the compressor or
any system component, the refrigerant charge
must be removed from both the high- and
low-pressure sides. Failure to do so may result in
serious personal injury. Pressure gauges must be
used to ensure all pressures are at atmospheric
level.
For more detailed information on the appropriate
materials required for brazing or soldering, please
contact the product manufacturer or distributor.
For specific applications not covered herein,
please contact Danfoss for further information.
System pressure testAlways use an inert gas such as nitrogen for
pressure testing. Never use other gasses such as
oxygen, dry air or acetylene as these may form
Maximum compressor test pressure (low side)33.3 bar (g)
Maximum compressor test pressure (high side)48.7 bar (g)
Maximum pressure difference between high and low
side of the compressor
Pressurize the system on HP side first then LP side
to prevent rotation of the scroll. Never let the
pressure on LP side exceed the pressure on HP
side with more than 5 bar.
36FRCC.PC.026.A4.02
an inflammable mixture. Do not exceed the
following pressures:
CH290 /CH485
37 bar (g)
On CH models which have an internal non return
valve in discharge fitting, we advise to pressurize
the system not quicker than 4.8 bar/s to allow
pressure equalization between LP and HP side
over scroll elements.
Application Guidelines
Installation
Leak detectionLeak detection must be carried out using a
mixture of nitrogen and refrigerant or nitrogen
and helium, as indicated in the table below.
Never use other gasses such as oxygen, dry air
Leak detection with refrigerantLeak detection with a mass spectrometer
Nitrogen and R410ANitrogen and Helium
Note 1: Leak detection with refrigerant may be forbidden in some countries. Check local regulations.
Note 2: The use of leak detecting additives is not recommended as they may affect the lubricant properties.
Vacuum evacuation and
moisture removal
Moisture obstructs the proper functioning of
the compressor and the refrigeration system. Air
and moisture reduce service life and increase
condensing pressure, and cause excessively high
discharge temperatures, which can destroy the
lubricating properties of the oil. Air and moisture
also increase the risk of acid formation, giving
rise to copper platting. All these phenomena
can cause mechanical and electrical compressor
failure.
For these reasons it’s important to perform a
vacuum dehydration on the system to remove
all residual moisture from the pipe-work after
assembly; CH compressors are delivered with <
or acetylene as these may form an inflammable
mixture. Pressurize the system on HP side first
then LP side.
100 ppm moisture level. The required moisture
level in the circuit after vacuum dehydration
must be < 100 ppm for systems with a CH.
• Never use the compressor to evacuate the
system.
• Connect a vacuum pump to both the LP & HP
sides.
• Evacuate the system to a pressure of 500 μm Hg
(0.67 mbar) absolute.
Do not use a megohm meter nor apply power to
the compressor while it’s under vacuum as this
may cause internal damage.
Filter driersA properly sized & type of drier is required.
Important selection criteria include the driers
water content capacity, the system refrigeration
capacity and the system refrigerant charge.
The drier must be able to reach and maintain
a moisture level of 50 ppm end point dryness
(EPD).
For new installations with CH compressors with
polyolester oil, Danfoss recommends using the
Danfoss DML (100% molecular sieve) solid core
filter drier. Molecular sieve filter driers with loose
beads from third party suppliers shall be avoided.
Refrigerant charging
For the initial charge the compressor must not
run and eventual service valves must be closed.
Charge refrigerant as close as possible to the
nominal system charge before starting the
compressor. This initial charging operation must
be done in liquid phase. The best location is on
the liquid line between the condenser outlet
and the filter drier. Then during commissioning,
when needed, a complement of charge can be
done in liquid phase: slowly throttling liquid in
on the low pressure side as far away as possible
from the compressor suction connection while
compressor is running. The refrigerant charge
quantity must be suitable for both summer and
For servicing of existing installations where acid
formation is present the Danfoss DCL (solid core)
filter driers containing activated alumina are
recommended.
The drier is to be oversized rather than under
sized. When selecting a drier, always take into
account its capacity (water content capacity),
the system refrigeration capacity and the system
refrigerant charge.
After burn out, remove & replace the liquid line
filter drier and install a Danfoss type DAS burnout
drier of the appropriate capacity. Refer to the DAS
drier instructions and technical information for
correct use of the burnout drier on the liquid line.
winter operations. Vacuum or charge from one
side can seal the scrolls and result in a nonstarting compressor. When servicing, always
ensure that LP/ HP pressures are balanced before
starting the compressor.
Be sure to follow all government regulations
regarding refrigerant reclamation and storage.
For more detailed information see
“Recommended refrigerant system charging
practice” news bulletin FRCC.EN.050.
37FRCC.PC.026.A4.02
Application Guidelines
Installation
Insulation resistance and
dielectric strength
Commissioning
Insulation resistance must be higher than 1
megohm when measured with a 500 volt direct
current megohm tester.
Each compressor motor is tested at the factory
with a high potential voltage (hi-pot) that
exceeds the UL requirement both in potential
and in duration. Leakage current is less than
0.5 mA.
CH scroll compressors are configured with
the pump assembly at the top of the shell,
and the motor below. As a result, the motor
can be partially immersed in refrigerant and
oil. The presence of refrigerant around the
motor windings will result in lower resistance
The system must be monitored after initial
startup for a minimum of 60 minutes to ensure
proper operating characteristics such as:
• Proper metering device operation and desired
superheat readings
• Suction and discharge pressure are within
acceptable levels
• Correct oil level indicating proper oil return
values to ground and higher leakage current
readings. Such readings do not indicate a faulty
compressor.
In testing insulation resistance, Danfoss
recommends that the system be first operated
briefly to distribute refrigerant throughout the
system. Following this brief operation, retest the
compressor for insulation resistance or current
leakage.
Never reset a breaker or replace a fuse without
first checking for a ground fault (a short circuit to
ground). Be alert for sounds of arcing inside the
compressor.
• Low foaming in sight glass and compressor
sump temperature 10K above saturation
temperature to show that there is no
refrigerant migration taking place
• Acceptable cycling rate of compressors,
including duration of run times
• Current draw of individual compressors within
acceptable values (max operating current)
• No abnormal vibrations and noise.
Oil level checking and
top-up
In installations with good oil return and line
runs up to 20 m, no additional oil is required. If
installation lines exceed 20 m, additional oil may
be needed. 1 or 2% of the total system refrigerant
charge (in weight) can be used to roughly define
the required oil top-up quantity but in any case
the oil charge has to be adjusted based on the oil
level in the compressor sight glass.
When the compressor is running under stabilised
conditions the oil level must be visible in the
sight glass.
The presence of foam filling in the sight glass
indicates large concentration of refrigerant in the
oil and / or presence of liquid returning to the
compressor.
The oil level can also be checked a few minutes
after the compressor stops.
When the compressor is off, the level in the
sight glass can be influenced by the presence of
refrigerant in the oil.
Always use original Danfoss POE oil 160SZ from
new cans.
Top-up the oil while the compressor is idle. Use
the schrader connector or any other accessible
connector on the compressor suction line and
a suitable pump. See News bulletin “Lubricants
filling in instructions for Danfoss Commercial
Compressors”.
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